AU652844B2

AU652844B2 - A process for the preparation of microspheres made of a biodegradable polymeric material

Info

Publication number: AU652844B2
Application number: AU20437/92A
Authority: AU
Inventors: Frederic Dr. Heimgartner; Piero Dr. Orsolini
Original assignee: Debio Recherche Pharmaceutique SA
Current assignee: Debio Recherche Pharmaceutique SA
Priority date: 1991-07-22
Filing date: 1992-07-21
Publication date: 1994-09-08
Anticipated expiration: 2012-07-21
Also published as: BE1005696A3; CA2074320C; NO922885D0; LU88151A1; IL102590A0; FR2680109A1; GR1001446B; FI923320A0; IT1259891B; FR2680109B1; BE1005697A5; RU2103994C1; FR2679450B1; GB2257909A; WO1993001802A1; IE69967B1; DK176218B1; FI106925B; DE4223282A1; HU218203B

Description

AUSTRALIA

Patents Act COMPLETE SPECIFICATION

(ORIGINAL)

'52844 Class Int. Class Application Number: Lodged: Complete Specification Lodged: Accepted: Published: Priority Related Art: 4**e 4* 4c Name of Applicant: DEBIO Recherche Pharmaceutique S.A.

Actual Inventor(s): Dr. Piero Orsolini Dr. Frederic Heimgartner Address for Service: PHILLIPS ORMONDE FITZPATRICK Patent and Trade Mark Attorneys 367 Collins Street Melbourne 3000 AUSTRALIA Invention Title: A PROCESS FOR THE PREPARATION OF MICROSPHERES MADE OF A BIODEGRADABLE POLYMERIC MATERIAL Our Ref 297972 POF Code: 106058/179253 The following statement is a full description of this invention, including the best method of performing it known to applicant(s): 6006 6006

A

A process for the preparation of microspheres made of a biodegradable polymeric material FIELD OF THE INVENTION A process for the preparation of a composition designed for the sustained and controlled release of medicamentous peptide substances, obtained in the form of microspheres of a biodegradable polymeric material incorporating said medicamentous substance.

SUMMARY OF THE INVENTION The process is aimed at providing a composition designed for the sustained and controlled release of medicamentous peptide substances, obtained in the form of microspheres of a biodegradable polymeric material S. incorporating said medicamentous substance.

It consists firstly in converting a water-soluble e. s cr~e e.

peptide or peptide salt into -awater-insoluble p;eptider -gpootivly peptide salt, then suspending said -peptieo, r:rsc potivcl peptide salt, in a solution of a biodegradable polymeric material, converting said suspension into an oil-in-water type enulsion, and f' ally isolating the microspheres of biodegradable po-ymer after transfer of the oil-in-water emulsion into an excess of an aqueous medium.

STATE OF THE ART Various solutions have been proposed to this day for the preparation of compositions capable of a sustained and a controlled release of medicamentous substances, making use of the manufacture of biodegradable implants, of microencapsulation or of the preparation of biodegradable porous matrices obtained for example as 2 microspheres or microparticles of various dimensions. In this respect, one can mention EP-A-0052510 for microencapsulation by phase separation of water-soluble drugs and EP-A-005848x or US-A-3976071 for the preparation of implants or of biodegradable porous matrices, based mainly on polylactide or on copolylactide-glycolide.

These techniques make use of a prior dissolution in an organic solvent of the biodegradable polymer or copolymer used as support and, if required, the dissolution of the medicamentous substance itself.

Other techniques, also capable of yielding microcapsules or microspheres, make use of emulsification procedures, the most important step of such procedures being the obtention of an oil-in-water type emulsion from an organic solution of polymeric material and an aqueous solutic of the peptide see in this respect US-A-4384975, 3891570, 4389330, 3737337, 4652441 or WO- 90/13361. In any case however, those versed in the art are obliged to develop techniques which are complex and difficult to control, in order to reduce as much as possible the losses of the highly water-soluble active peptide substances, such as for example a double eiulsification.

THE INVENTION In a process using the formation of an emulsion of the oil-in-water type followed by its transfer into an aqueous medium, the invention enables, against all expectations, to overcome advantageously the shortcommings of techniques known to this day.

Actually, by firstly proceeding to the conversion of a water-soluble peptide or peptide derivative into a water-insoluble ppti d, roc'pekvfy. peptide salt, the invention makes available to those versed in the art, quite a novel means of taking advantage of the relative y 4 A solubilities of the ingredients which are used and in 3 particular of the.solvents and "non-solvents" involved.

PREFERRED EMBODIMENTS OF THE INVENTION More particularly, the object of the invention is a process which is characterized by the fact that a. a water-soluble peptide or peptide salt is converted into -i4 water-insoluble paptid s a i peptide salt; b. said water-insoluble 3nQ. GFka, peptide salt, is suspended in an organic medium containing the biodegradable polymeric material in the dissolved state; c. said organic suspension is dispersed in an S. aqueous medium forming the continuous phase of the resulting emulsion; 9* d. said emulsion is transferred into an excess of an aqueous medium, and finally the microspheres thus obtained are separated from the liquid phase.

In the invention, "medicamentous peptide substance", is used to designate primarily a natural or a synthetic polypeptide, which is physiologically active and which comprises from 3 to 45 amino acids. The range of polypeptides which can be treated in accordance with the process of the invention is quite extensive and includes in particular oxytocin, vasopressin, corticotrophin, calcitonin, epidermal growth factor (EGF), prolactin, inhibitin, interferon, somatostatin, insulin, glucagon, auricular natriuretic factor (ANF), endorphin, a renin inhibitor, luteinizing hormone-releasing hormone (LHRH), growth hormone releasing hormone (GIIRH), peptide T or one of their synthetic analogues or homologues.

Preferably, one can mention polypeptides such as LHRH or somatostatin, or one of their synthetic homologues or analogues, such as -4 D-Phe-Cys -Phe-D-Trp-Lys-Thr-Cys -Thr-OH, D-Phe-Cys-Phe-D-Trp-Lys-Thr-Cys-Trp-NHi 2 D-Trp-Cys-Phe-D-Trp-Lys-Thr-Cys-Thr-NH 2 D-Phe-Cys--Tyr-D-Trp-Lys-Val-Cys-Thr-NH 2 D-Phe-Cys--Tyr-D-Trp-Lys-Val-Cys-Trp-NH 2 AcPhe-Cys-Phe-D-Trp-Lys-Thr-Cys-Thr-NH 2 AcPhe-Cys-Tyr-D-Trp-Lys-Val-C's-Trp-NH 2 Ac-DNal-DpCl-Phe-DPal-Ser-Tyr-DCit-Leu-Arg-Pro-DAla-NH 2 (pyro) Glu-His-Trp-Ser-Tyr-D-Trp-Leu-Arg-Pro-Gly-NH 2 (pyro) Glu-His-Trp-Ser-Tyr-D-Phe-Leu-Arg-Pro-Gly-NH 2 (pr)l*isTpDSr-y--e-LuAgPoVl-H1 (pyro) Glu-His-Trp-DSer-Tyr-D-Le-Leu-Arg-Pro-Gly-HR 1

(R

1 lower alkyl).

This list is however not exhaustive.

:The first phase of the process consists in converting, by means of conventional techniques, a watersoluble peptide or peptide salt into a water-insoluble peptide, respectively peptide salt. By "water-soluble" is meant a peptide or a peptide derivative having a water solubility in excess or equal to 0.1 mg/ml at 0 C, preferably in excess or equal to 1.0 mg/ml.

By "water-insoluble" is meant a peptide or a peptide derivative having a water solubility lesser or equal to 0.1 mg/ml at 25 0 C. Peptide salts such as pamoate, tannate, stearate or palmitate satisfy this definition.

As to the biodegradable polymeric material, the 5 most commonly used are polymers such as a polylactide, a polyglycolide, a copolymer of lactic and glycolic acids, a polyester such as a polyalkylene fumarate or succinate or further a polyorthoester, a polyacetal or a polyanhydride.

Amongst the preferred polymeric materials, one should mention the copolymers of lactic and glycolic acids (PLGA) and in particular the copolymers of L- or D,L-lactic acid containing from 45 to 90% (molar) of lactic acid units and respectively 55 to 10% (molar) of glycolic acid units.

One can also mention in this respect various polyalkylene fumarates or succinates, and in particular the poly-1,4-butylene-succinate, the poly-2,3-butylene succinate, the poly-l,4-butylene fumarate or the poly- 2,3-butylene fumarate. These polymers are readily prepared as described in the literature or can be obtained from specialized firms.

As to the solvent selected for the polymeric material, one can use an organic solvent such as for example methylene chloride, but in any case, the solvent must be a "non solvent" for the selected peptide or peptide salt.

According to the invention, once said peptide or oo salt is suspended in the organic solution of the poly- S. meric material, this solution is incorporated into a predetermined amount of an aqueous medium, most generally of water complemented with an appropriate surfactant.

The objective is to form rapidly a homogeneous emulsion of the oil-in-water type, said aqueous medium functioning to provide the continuous phase. Various factors are to be considered when preparing such an emulsion, which in turn influence the size or the structure of the microspheres resulting from the process. One of the factors which must be taken into consideration is the rate of addition of the organic solution to the aqueous medium; another one can be the temperature or further the agitation speed or the energy of dispersion (ultrasonic treatment), with the last mentioned parameter influencing in particular the size of the final microspheres. It is within the capacity of those versed in the art to select the methods and the conditions of emulsification suitable for achieving the intended purpose.

In the preparation of said emulsion, it may also prove advantageous to modify the volume ratio of the phases in contact, in particular to decrease the initial volume of the organic phase with respect to that of the aqueous phase. In some cases, owing to the volatility of *the organic solvents which are used for example methylene chloride the evaporation occurring spontaneously during agitation may already prove sufficient; •go• in other cases, this desirable phenomenon may be accelerated by proceeding to a partial evaporation, under reduced pressure.

Once the organic-aqueous emulsion has been stabilized, it is transferred into an excess amount of an aqueous medium, most generally water. The purpose of this operation is to intensify the hardening of the embryonic microspheres formed in the emulsion, by extracting the organic solvent still remaining inside said microspheres. This operation is also aimed at elimina- S".ting at the same time trace amounts of surfactant which may have remained in the body of the polymer during its final hardening phase. It is to be noted, that water is a "non-solvent" for both the biodegradable polymeric material such as PLGA for example and for the peptide salt trapped inside said microspheres. This situation is particularly favourable for the indispensable extraction of the residual polymer solvent, such as for example

CH

2

C

2 Having transferred said emulsion into an excess of an aqueous medium, the hardened microspheres are collected using conventional techniques, for example by 7 centrifugation, filtration or by gravity settling. The same applies to the washing, purification and drying operations.

One of the advantages of the process of the invention is that it makes it possible to obtain microspheres the size of which can be accurately controlled, this control taking place mainly during the preparation of the emulsion (agitation speed for example). Another advantage is that a particularly high peptide loading can be achieved, amounting to 5, 10 or 20% in weight, or even higher, depending on conditions. Further, the yield of the peptide or peptide salt incorporation is particularly high; this is due mainly to the prior conversion of the selected peptide from a water-soluble derivative into a water-insoluble derivative, such as a salt for example.

The microspheres obtained according to the process of the invention from the above-mentioned ingredients are then used after being appropriately sterilized, for the preparation of suspensions used in parenteral administration, for example by intramuscular or subcutaneous injection.

2. The invention is illustrated by the fol ing examples. The substances and the operational c ditions used in these examples do not limit the inve ion in any way.

Example 1 3 g of the acetate of -Trp6-LHRH of the formula (pyro)Glu-His-Trp-S -Tyr-D-Trp-Leu-Arg-Pro-Gly-NH2 were convert into the corresponding pamoate, using conventio techniques. After comminution, this salt appear as formed of microparticles of an amorphous iALq st cture with an average particle size of approximate- 7A Any suitable medicamentous substances may be incorporated into the composition prepared by the process of the invention. For example the medicamentous substance may be selected from oxytocin, vasopressin, corticotrophin, calcintonin, epidermal growth factor (EGE), prolactin, inhibitin, interferon, somatostatin, insulin, glucagon, auricular natriuretic factor (ANF), endorphin, a renin inhibitor, luteinizing hormone-releasing hormone (LHRH), growth hormone releasing hormone (GHRH), peptide T or one of their synthetic analogues or homologues.

In a preferred embodiment of the medicamentous substance is LHRH or somatostatin, or one of their synthetic analogues or homologues, soiected from D-Phe-Cys-Phe-D-Trp-Lys-Thr-Cys-Thr-OH, 15 D-Phe-Cys-Phe-D-Trp-Lys-Thr-Cys-Trp-N H 2 D-Trp-Cys-Phe-D-Trp-Lys-Thr-Cys-Thr-N H 2 D-Phe-Cys-T yr-D-Trp-Lys-VaI-Cys-Thr-NH2, D-Phe-Cys-Tyr-D-Trp-Lys-Val-Cys-Trp-N H 2 AcPhe-Cys-Phe-D-Trp-Lys-Thr-Cys-Thr-N H 2 AcPhe-Cys-Tyr-D-Trp-Lys-Val-Cys-Trp-N H 2 Ac-DNaI-DpCi-Phe-DPal-Ser-Tyr-DCit-Leu-Arg-Pro-DAla-NH 2 (pyro)Glu-His-Trp-Ser-Tyr-D-Trp-Leu-Arg-Pro-Gly-NH 2 (pyro)Glu-His-Trp-Ser-Tyr-D-Phe-Leu-Arg-Pro-Gly-NH 2 (pyro)Glu-His-Trp-D-Ser-Tyr-D-Leu-Leu-Arg-Pro-Gly-NH R', ~ALI (pyro) Glu-H is-Trp-Ser-Tyr-D-Trp-Leu-Arg-Pro-N HR 1 r~,1 11,3 lower alkyl).

-7B The invention is illustrated by the following examples. The substances and the operational conditions used in these examples do not limit the invention in any way.

Example 1 3 g of the acetate of D-Trp6-LHRH of the formula: (pyro)Glu-His-Trp-Ser-Tyr-D-Trp-Leu-Arg-Pro-Gly-NH 2 were converted into the corresponding pamoate, using conventional techniques. After comminution, this salt appears as formed of microparticles of 15 an amorphous structure with an average particle size of approximate- :e «o *o 8 ly 10 microns. Solubility lesser than 0.025 mg/ml in at 40 0

C.

0.280 g of the pamoate of D-Trp 6 -LHRH were then suspended in 20 ml of CH 2 C12, and said suspension was added to 20 ml of CH 2 C1 2 containing 1.720 g of dissolved copolymer of D,L-lactic and glycolic acids (PLGA) 75:25 (molar inherent viscosity of 0.82 in HFIP).

The mixture was prepared at room temperature, under stirring, to obtain a suspension which was perfectly homogeneous.

The resulting suspension was then poured, in one portion, into 500 ml of water containing 0.075% dissolved methoxycellulose and stirring of the mixture was continued for about 90 min. at room temperature (speed of agitation 900 rpm). The evolution of the emulsion was monitored at regular intervals of time, on the average every 30 minutes, by taking a sample and examining the microspheres obtained with a microscope.

Once the stirring is ended (stabilization of the size reduction of the microspheres), said emulsion is transferred in one portion into 2 1 of water maintained at approximately 10 0 C, while stirring the mixture until homogenization.

The iicrospheres of PLGA were isolated from the reaction mixture and purified by successive centrifugations alternating with washings with H 2 0, and finally filtered and dried und-r reduced pressure. 1.25 g of PLGA microspheres were thus collected (yield 63%), which included more than 96% particles having a diameter lesser than 100 microns (maximum at 55-85 microns).

The analysis (dissolution of the solid PLGA, extraction and determination of the peptide by HPLC) shows that the loading of the pamoate of D-Trp 6 -LHRH of the microspheres amounts to 9.05% in weight (theoretical The microspheres thus obtained were subsequently subjected to a sterilization by gamma rays and suspen- 9 ded in an appropriate sterile vehicle. In vivo tests (determination of the blood testosterone level in male rats) confirmed the regular release of the active substance over at least 21 days, producing from D4 (injection at DO) a collapse of the testosterone level to values typical of castrated animals.

TIME (days) TESTOSTERONE (ng/ml) 9. *9 0 0 0e 0 0*0* *0 0 0* 00 0 0* 0* 0 *00 0 3.7 2 5.1 4 0.7 7 0.6 11 0.8 14 1.2 18 1.9 21 25 Example 2 Exactly the same procedure was used as in Example 1, except that 0.560 g of the pamoate of D-Trp 6

-LHRH

were used for 1.440 g of PLGA 75:25 (molar 1.49 g of PLGA microspheres were collected (yield and they included more than 90% particles having a diameter lesser than 100 microns.

Level of loadir,' 16.3% in weight (theoretical Example 3 The same procedure was used as in Example 1, starting with 0.140 g of the pamoate of D-Trp 6 -LHRH and 10 0.860 g of poly-1,4-butylene succinate (inherent viscosity in HFIP, approximately 0.35).

The resulting organic-aqueous emulsion was transferred in one portion into 500 ml of water and the resulting mixture was subjected to successive centrifugation and H 2 0 washing treatments, filtration and finally drying under reduced pressure to produce 0.52 g (yield 52%) of polysuccinate microspheres.

Level of loading 2.87% in weight (theoretical Example 4 SFirstly, the acetate of an analogue of somatostatine of the formula D-Phe-Cys-Tyr-D-Trp-Lys-Val-Cys-Trp-NH 2 8 was converted into the corresponding pamoate using conventional techniques, to obtain particles having an average size of approximatively 10 microns.

0.266 g of said pamoate and 1.734 g of PLGA 75:25 (molar were then used according to the procedure c' Example 1. After pouring the organic-aqueous emulsion into 2 1 of H 2 0 at 10°C, homogenization, centrifugation and the same subsequent treatments as described above, 1.23 g (yield 62%) of PLGA microspheres were collected, which included more than 98% particles having a diameter lesser than 100 microns (maximum at 40-65 microns).

Level of loading 8.7% in weight (theoretical 11 a a S*

S

S* S S a.

S a SO

S

Example Exactly the same procedure was used as in Example 4, with 0.532 g of the pamoate of the somatostatin analogue, for 1.468 g of PLGA 75:25.

Microspheres of PLGA 1.21 g (yield Level of loading 17.5% in weight (theoretical The microspheres thus obtained, sterilized by means of gamma rays, were finally suspended in an appropriate sterile vehicle. In vivo tests (determination of the blood serum level of the somatostatine analogue in rats which had received one injection at JO) confirm a controlled release of a detectable amount of active substance over a period of 20 days (injection IM).

TIME (days) DETERMINATION OF PEPTIDE (ng/ml) 0 3 hours 64.0 1 15.0 2 10.0 3 6 8 14 16 Example 6 3 g of the acetate of a LHPH analogue of the 12 formula Ac-D-Nal-D-pCl-Phe-D-Pal-Ser-Tyr-D-Cit-Le-Arg-Pro-D-AlaNH 2 were converted into the corresponding pamoate by conventional techniques and treated in such a manner as to obtain particles having an average size of approximately microns.

0.317 g of said pamoate and 1.683 g of PLGA 75:25 (molar were subsequently treated according to the procedure of Example 1, to produce finally 1.61 g (yield 80%) of PLGA microspheres including more than 94% particles having a diameter lesser than 100 microns S(maximum at 55-85 microns).

4 4 4 Level of loading 9.05% in weight (theoretical oo" 44 Example 7 Exactly the same procedure was used as in Example 6, with 0.634 g of the pamoate of the LHRH analogue, for 1.366 g of PLGA 75:25.

PLGA microspheres 1.70 g (yield Level of loading 18.3% (theoretical The microspheres thus obtained were subsequently subjected to a gamma ray sterilization and suspended in an appropriate sterile vehicle. In vivo tests (determination of the blood serum level of the analogue in male rats) confirm the regular release of a biologically significative amount of active substance over at least 24 days.

13 TIME (days) DETERMINATION OF PEPTIDE (ng/ml) 0 3 hours 47.1 1 48.9 2 52.2 3 46.9 6 50.4 8 40.1 42.1 14 29.8 16 33.5 20 33.0 .24 25.6 These results are further confirmed by analyses carried out on subjects sacrificed at D30 loss of weight of the testes of at least 80%, loss of weight of the seminal vesicles of at least Example 8 Exactly the same procedure was used as in Example 1, starting with 0.05 g of the pamoate of salmon calcitonin and 1.0 g of copolymer of D,L-lactic/glycolic acids 50:50 (molar The conventional in vivo tests confirm a controlled release of the active substance over a period of approximately 8 days.

13A- The claims defining the invention are as follows: 1. Process for the preparation of a composition designed for the sustained and controlled release of medicamentous peptide substances, obtained in the form of microspheres of a biodegradable polymeric material incorporating said medicamentous substance, characterized in that a) a water-soluble peptide or peptide salt is converted into the respective water-insoluble peptide salt; b) said water-insoluble peptide salt, is suspended in an organic medium containing the biodegradable polymeric material in the dissolved state; c) said organic suspension is dispersed in an aqueous medium forming the continuous phase of the resulting emulsion; d) said emulsion is transferred into an excess of an aqueous medium, and finally the microspheres thus obtained are separated from the 15 liqc;.id phase.

*eee

Claims

09.60:(pyro) Glu-His-Trp-Ser-Tyr-D-Trp-Leu-Arg-Pro-Gly-NH 2 *0 (pyro) Glu-His-Trp-Ser-Tyr-D-Phe-Leu-Arg-Pro-Gly-NH 2 (pyro) Glu-His-Trp-D-Ser-Tyr-D-Leu-Leu-Arg-Pro-Gly-NHR 1 or (pyro) Glu-His-Trp- Ser-Tyr-D-Trp-Leu-Arg-Pro-NHR 1 (R 1 lower alkyl). Process according to claim 5, characterized in that the water-insoluble peptide salt is a pamoate, a tan- nate, a stearate or a palmitate. Process according to one of claims 1 to 6, c-harac- terized in that the biodegradable polymeric mnaterial is -16- a polyactide, a polyglycolide, a copolymer of lactic and glycolic acids, a polyester such as a polyalkylene fumarate or succinate or further a polyorthoester, a polyacetal or a polyanhydride. 8. Process according to claim 7, characterized in that the copolymer of lactic and glycolic acids is a copolymer of L- or D,L-lactic acid containing from to 90% (molar) of lactic acid units and respectively 55 to 10% (molar) of glycolic acid units. 9. Process according to claim 8, characterized in that the polyalkylene fumarate or succinate is a poly-1,4-butylene-succinate, a poly-2,3-butylene succinate, a poly-1,4-butylene fumarate or a poly-2,3-butylene fumarate. Process according to claim I substantially as hereinbefore described with reference to any one of the examples. 15 DATED: 7 July 1994 PHILLIPS ORMONDE FITZPATRICK Attorneys for: DEBIO RECHERCHE PHARMACEUTIQUE S.A. 00 0000* 17 ABSTRACT The process is aimed at providing a composition designed for the sustained and controlled release of medicamentous peptide substances, obtained in the form of microspheres of a biodegradable polymeric material incorporating said medicamentous substance. It consists in converting first a water-soluble peptide or peptide salt into a water-insoluble peptide, respectively peptide salt. The following steps include preparing an organic-aqueous emulsion and then extrac- ting the organic solvent in an excess of aqueous medium. b S S S